US2023083041A1PendingUtilityA1

Electrochemical conversion

Assignee: UNIV CALIFORNIAPriority: Apr 1, 2019Filed: Mar 31, 2020Published: Mar 16, 2023
Est. expiryApr 1, 2039(~12.7 yrs left)· nominal 20-yr term from priority
Y02P20/133C25B 11/085B01J 31/1815C25B 11/065B01J 2531/74C25B 1/23C25B 11/054B01J 31/20
43
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Claims

Abstract

The present disclosure provides methods, compositions, devices, systems and uses that pertain to the electrochemical reduction of CO2 to CO. The application presents a class of electrodes, incorporating molecular catalysts in nanostructures, for robust and efficient electrochemical systems, specifically, selective and robust hybrid electrodes, by incorporating a rhenium (Re) catalyst into the structure of highly porous heterogeneous materials. These electrodes can be scaled up to desired manufacturing dimensions due to their robust nature and methods of preparation.

Claims

exact text as granted — not AI-modified
1 . A composition comprising a rhenium catalyst and a carbon support wherein:
 the rhenium catalyst has a formula of Re(4,4′-R-2,2′-bipyridine)(CO) 3 X;   R is an electron donating group or an electron withdrawing group;   X is a halogen, acetonitrile, CH 3 CN(OTf), or Py(OTf); and   wherein the rhenium catalyst is dispersed on a surface of the carbon support.   
     
     
         2 . The composition of  claim 1 , wherein the carbon support is multi-walled carbon nanotubes. 
     
     
         3 . The composition of  claim 1 , wherein X is a halogen. 
     
     
         4 . The composition of  claim 1 , wherein X is chloro. 
     
     
         5 . The composition of  claim 1 , wherein R is an electron donating group. 
     
     
         6 . The composition of  claim 1 , wherein the rhenium catalyst is Re(tBu-bpy)(CO) 3 Cl. 
     
     
         7 . The composition of  claim 1 , wherein R is an electron withdrawing group. 
     
     
         8 . The composition of  claim 1 , wherein the composition is characterized by a current density of at least about 4 mA/cm 2 . 
     
     
         9 . The composition of  claim 1 , wherein the composition is characterized by a current density of about 4 mA/cm 2 . 
     
     
         10 . The composition of  claim 1 , wherein the composition is characterized by a turnover number (TON) greater than about 5600 and a turnover frequency (TOF) greater than about 1.6 s −1 . 
     
     
         11 . A method for electrocatalytically reducing CO 2  to CO, comprising: contacting an electrode with CO 2 ;
 wherein the electrode is in an aqueous solution having a pH of at least 4, comprising an electrolyte;   wherein the electrode comprises the composition of  claim 1 ; and   wherein the method is performed at a temperature of at least about 5° C.   
     
     
         12 - 18 . (canceled) 
     
     
         19 . The method of  claim 11 , wherein the selectivity for CO over H 2  is at least about 99%. 
     
     
         20 . The method of  claim 11 , wherein the selectivity for CO over H 2  is from about 30% to about 100%. 
     
     
         21 . The method of  claim 11 , wherein the method is characterized by a Faradaic efficiency of at least about 99%. 
     
     
         22 . The method of  claim 11 , wherein the electrolyte comprises KHCO 3 . 
     
     
         23 . The method of  claim 11 , wherein the method is performed at a temperature of from about 5° C. to about 35° C. 
     
     
         24 . (canceled) 
     
     
         25 . The method of  claim 11 , wherein the pH of the aqueous solution is from about 6 to about 8. 
     
     
         26 - 30 . (canceled) 
     
     
         31 . A process for preparing an electrode, comprising:
 suspending a rhenium catalyst, a carbon support, and carbon nanofiber in ethanol to form a suspension;   sonicating the suspension;   drop-casting the suspension onto a glassy carbon plate to form a drop-casted glassy carbon plate;   drying the drop-casted glassy carbon plate at a temperature from about 100° C. to about 180° C. for about 0.5 to about 24 hours; and   wherein the rhenium catalyst is the rhenium catalyst according to  claim 1 .   
     
     
         32 - 39 . (canceled) 
     
     
         40 . The process of  claim 31 , wherein the suspension is drop-casted at a temperature from about 40° C. to about 80° C. 
     
     
         41 . (canceled) 
     
     
         42 . The process of  claim 31 , wherein the drop-casted glassy carbon plate is dried at a temperature of about 150° C. for about 1 hour. 
     
     
         43 . (canceled)

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